FDFCC-Ⅲ工艺加工焦化汽油的工业实践
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  • 英文篇名:The Application of FDFCC-Ⅲ Process in Processing Coker Naphtha
  • 作者:赵赞立 ; 孟凡东 ; 闫鸿飞 ; 段少魏 ; 张亚西
  • 英文作者:Zhao Zanli;Meng Fandong;Yan Hongfei;Duan Shaowei;Zhang Yaxi;Jiangsu Xinhai Petrochemical Group Co.,Ltd.;SINOPEC Engineering (Group) Co.,Ltd.,SEG;
  • 关键词:催化裂化 ; 焦化汽油 ; 改质 ; 辛烷值 ; 脱硫
  • 英文关键词:catalytic cracking;;coker naphtha;;upgrading;;octane value;;sulfur removal
  • 中文刊名:SYZW
  • 英文刊名:Sino-Global Energy
  • 机构:江苏新海石化有限公司;中国石化炼化工程(集团)股份有限公司;
  • 出版日期:2015-08-15
  • 出版单位:中外能源
  • 年:2015
  • 期:v.20
  • 语种:中文;
  • 页:SYZW201508025
  • 页数:4
  • CN:08
  • ISSN:11-5438/TK
  • 分类号:90-93
摘要
焦化汽油辛烷值低、安定性差,烯烃和硫含量高,不能作为汽油的调合组分直接出厂。随着国家对环境保护的日益重视,对汽油的质量要求不断提高,需要采用简单易行的加工方法对焦化汽油进行改质,提高其辛烷值、降低烯烃和硫含量,同时加工损失又较小。中国石化洛阳工程公司研发的FDFCC-Ⅲ工艺,由于设置第二提升管,对于加工焦化汽油具有独特优势。第二提升管为焦化汽油催化改质反应提供了独立的反应场所,可以灵活、多方案地实现焦化汽油的加工。在改质反应温度550℃条件下,焦化汽油经第二提升管改质后,汽油保留率为72.78%,液化石油气+改质汽油+柴油收率为94.44%,焦炭产率为2.21%,干气产率为2.72%。同时汽油性质得到明显改善,RON辛烷值提高11个单位,脱硫率达到78.0%,脱氮率达到91.8%,且改质汽油烯烃含量大幅度下降,诱导期延长,为焦化汽油的利用提供了一条简单易行的工艺路线。
        Coker naphtha has low octane value,poor safety and high contents of olefin and sulfur and therefore cannot be directly used as a gasoline blending component.As it attaches increasing importance to envi-ronmental protection,China has increasingly strict requirements for the quality of gasoline.Refiners need to up-grade coker naphtha to increase its octaine value,reduce olefin and sulfur contents and lower processing loss using simple and easy procesing methods.The FDFCC- Ⅲ process developed by Sinopec Luoyang Engineering Company has its unique advantages over other similar products when used for processing coker naphtha as it is equipped with a second riser.The addition of the second risr has provided a standalone reaction place for the catalytic upgrade of coker naphtha,enabling flexible and multiple ways of coker naphtha processing.When the reaction temperature is 550 ℃,the gasoline retention rate after coker naphtha was upgraded through the second riser reaches 72.78%,the combined yield of LPG,upgrade gasoline and diesel fuel is 94.44%,the coke yield is 2.21% and the dry gas yield is 2.72%.The properties of gasoline improved considerably — RON increased by 11 units,78.0% of sulfur was removed,and 91.8% of nitrogen was removed.In addition,the content of olefin in the upgraded gasoline dropped significantly and the induction period extended.The up-grade has offered a simple and easy route for the utilization of coker naphtha.
引文
[1]孟凡东,黄延召,王龙延,等.低温接触、大剂油比的催化裂化技术[J].石油炼制与化工,2011,42(6):34-39.
    [2]陈曼桥,孟凡东.增产丙烯和生产清洁汽油新技术——FDFCC-Ⅲ工艺[J].石油炼制与化工,2008,39(9):1-5.
    [3]陈俊武,曹汉昌.催化裂化工艺与工程[M].北京:中国石化出版,2005.
    [4]闫鸿飞.FDFCC-Ⅲ工艺汽油提升管汽油降硫影响因素研究[J].河南化工,2010,27(19):47-49.
    [5]赵日峰.焦化汽油进催化装置提升管反应器改质技术分析[J].金陵石油化工,1997(2):37-39.
    [6]张国才.焦化汽油的催化裂化改质[J].石油炼制与化工,2001,32(4):5-9.

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